[go: up one dir, main page]

CN1036232A - A kind of complex carburizer - Google Patents

A kind of complex carburizer Download PDF

Info

Publication number
CN1036232A
CN1036232A CN89101219A CN89101219A CN1036232A CN 1036232 A CN1036232 A CN 1036232A CN 89101219 A CN89101219 A CN 89101219A CN 89101219 A CN89101219 A CN 89101219A CN 1036232 A CN1036232 A CN 1036232A
Authority
CN
China
Prior art keywords
carburizing
kerosene
carburizer
complex
rare earth
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
CN89101219A
Other languages
Chinese (zh)
Other versions
CN1010788B (en
Inventor
刘跃
汪伯华
郦振声
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuhan Research Institute of Materials Protection
Original Assignee
Wuhan Research Institute of Materials Protection
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wuhan Research Institute of Materials Protection filed Critical Wuhan Research Institute of Materials Protection
Priority to CN88107570A priority Critical patent/CN1010788B/en
Publication of CN1036232A publication Critical patent/CN1036232A/en
Publication of CN1010788B publication Critical patent/CN1010788B/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/20Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone
    • F23D14/22Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B9/00Stoves for heating the blast in blast furnaces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2900/00Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/21Burners specially adapted for a particular use
    • F23D2900/21001Burners specially adapted for a particular use for use in blast furnaces

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)

Abstract

A kind of by the kerosene that dissolves each other, the complex carburizer that pure and mild rare earth element is formed, be suitable for the drop-feeding gas carburization and the vacuum ionic carburization of pit gas carburizing furnace, be particularly suitable for the controlled atmosphere carburizing of pit carburizing furnace, make single factor controlled atmosphere carburizing carbon-potential control precision≤± 0.05%, no carbon black, carburizing speed is higher than kerosene, carburizing oil, acetone and a vinyl acetic monomer.

Description

A kind of complex carburizer
The invention belongs to the thermo-chemical treatment field.
Pit furnace drop-feeding gas carburization technology is one of processing method the most frequently used in the domestic and international mechanical industry.The quality of carburizing part quality is related to the quality and the work-ing life of engineering goods.The carburizing part surface carbon concentration is low, will reduce the contact fatigue strength and the fatigue strength of workpiece surface.Carbon contents is too high, then easily produces the netted or massive carbide in surface, increases surface brittleness.Carburizing part top layer carbon content is to have surface generalization mechanical property preferably at 0.9~1.0% o'clock, the main path of control carburizing part quality is according to different actual service conditionss, the carbon content of control cementation zone, for drop-feeding gas carburization, the carbon potential of necessary controlled atmosphere.Influencing one of carburizing atmosphere carbon-potential control accuracy factors is that can the furnace gas composition be stablized, and the stability of furnace gas composition is directly relevant with the degradation production of instillation again.
The carburizing process method of at present external (as Europe and Japan) widespread use is the rich mug(unit of measure) method (Carbomaag) of so-called card.The rich mug(unit of measure) method gas cementation of card is two kinds of organic liquids directly to be splashed into carry out cracking in the pit furnace and prepare carburizing atmosphere.These two kinds of organic liquids, a kind of is that another kind is ethyl acetate or acetone for the methyl alcohol of carrier gas and dilution usefulness, they are the cracked carburizing atmosphere under carburizing temperature, the furnace gas ingredient stability, the carburizing quality is good, carries out the controlled atmosphere carburizing easily.In view of the particular case of China, acetone, the cost of vinyl acetic monomer is higher, so the most manufacturers of China adopt illuminating kerosene to make carburizing agent.Its advantage is a low price, and carburizing speed is fast.But kerosene belongs to fatty hydrocarbon polymer, its constituent structure instability, and because of the place of production different different.Kerosene is pressed following formula substantially and is decomposed under carburizing temperature (920 ℃)
CnH 2n+2n〔C〕+(n+1)H 2n=9-16
Since there is not carbon monoxide in the cracking component of kerosene, the carbon monoxide in the kerosene cracking atmosphere that carburizing is produced as instillation, and the oxygen that remains in the stove after mainly finishing by exhaust cycle forms.Along with the continuity of carburizing time, the carbon monoxide in the furnace gas reduces gradually, and the each component content is big, and superfluous carbon will cause forming carbon black.At this situation, available kerosene+air, the method for kerosene+water suitably increases oxygen in the stove, and the fluctuation that solves carbon monoxide in the kerosene splitting gas is excessive, the problem that excess carbon is too many.The people is also arranged, as yellow bright proposition the " proportioning kerosene " technology of taking of Guangdong Machinery College, but this article author fails to solve methyl alcohol and the immiscible problem of kerosene, and adopting mechanism such as electromagnetic valve flowmeter, the flow proportional by adjusting two kinds of liquid also makes it flow into simultaneously that the cracked method constitutes " proportioning " kerosene in the cementing furnace.This proportioning kerosene requires methyl alcohol and kerosene to splash in the stove by different flow simultaneously respectively with two pipelines when realizing this technology.The ratio of flow must be by under meter control, the mobile effect that is subjected to self gravitation of liquid, and change with level change, because the fluctuations in discharge of the frequent variation of flow and two kinds of liquid is asynchronous, institute is so that the operator when realizing this technology, has all inconvenience.
Make the existing the problems referred to above of carburizing agent in order to solve with kerosene, the present invention is basic foundation with delivery of supplemental oxygen part in kerosene equally, by selecting suitable alcohols and rare earth element for use, realize dissolving each other of itself and kerosene, impel the abundant cracking of kerosene and stablize carbon monoxide content in its cracking atmosphere, obtained success.
Complex carburizer of the present invention is by the kerosene that dissolves each other, pure and mild rare earth element is formed, its composition is for containing kerosene 60~80%, alcohol 20~40% and rare earth element 0.3~0.6%(be % by weight all), said pure carbonaceous sources subnumber preferably 1~7, said rare earth element is cerium and/or lanthanum preferably.Pure and mild rare earth coal supply oil subsidy in the complex carburizer of the present invention fills suitable oxygen, and making increases the stable of carbon monoxide and cracking atmosphere in its cracking component, and can reduce the excess carbon of kerosene, makes the methane (HH in the furnace gas component 4) content keep appropriate value.Rare earth element has very big effect to improving carburizing speed, and this is because rare earth element easily makes the workpiece surface iron oxide reduction, clean workpiece surface; The carburizing of rare earth element goes into to reduce crystal boundary energy, makes the austenite crystal refinement, and owing to grain refining, crystal boundary increases, and has quickened the diffusion of carbon atom in steel in cementation process; The atomic radius of rare earth element is bigger, and its infiltration makes the lattice constant of infiltration layer that bigger variation take place, and this lattice distortion helps carbon atom in gathering partially that distortion is distinguished, and causes surface carbon concentration to improve, thereby quickens the diffusion of carbon.Complex carburizer of the present invention can be used for single drop and annotates carburizing, also can carry out carburizing with common instillation of methyl alcohol biliquid.
Advantage of the present invention:
1. the fluctuation of each component content is little in this complex carburizer cracking atmosphere, ingredient stability.
2. this complex carburizer carburizing speed is fast, improves carburizing speed 10~15% than the kerosene penetration enhancer.
3 complex carburizer carburizings energy force rate kerosene of the present invention are strong, and the available quantity of carbon is bigger than kerosene, so under the same terms, the consumption of carburizing agent is little.
4. complex carburizer of the present invention, the controlled carburizing of formula pit furnace list factor that is used to instil can guarantee carbon-potential control precision≤0.05%, single liquid or biliquid instillation carburizing in pit furnace, carbon monoxide content fluctuation range≤± 1%, methane content is suitable, and deposition of soot is few.
5. this carburizing agent is stable, puts for a long time under the normal temperature not have and decomposes.
Embodiment 1:
With the present invention's complex carburizer, contain kerosene 75%, Virahol 23~24%, propyl carbinol 1% and rare earth element 0.3%(be % meter by weight all).
920 ℃ of carburizing temperatures, 4 hours time
The grade of steel of carburizing treatment: 20CrMnTi 20 #Steel
Alloying layer thickness: 1.05mm(20CrMnTi)
0.75mm(20 #Steel)
Hardness after the hardening: HRC60~62
Cementing furnace: RJJ-75
Drip amount: 120 droplets/minute
Embodiment 2:
With the multiple complex carburizer of the present invention, contain kerosene 80%, n-propyl alcohol 17~18%, isopropylcarbinol 2%, rare earth element 0.6%(be % meter by weight all).
920 ℃ of carburizing temperatures, 5.5 hours time
The grade of steel of carburizing treatment: 20CrMnTi 20Cr
Alloying layer thickness: 1.2mm(20CrMnTi)
1.1mm(20Cr)
Hardness after the hardening: HRC60~61
Cementing furnace: RJJ-75
Drip amount: 130 droplets/minute
Embodiment 3:
With the present invention's complex carburizer, contain kerosene 68~72%, Virahol 25~30%, primary isoamyl alcohol 0.8~2%, rare earth element 0.5%, (all % counts by weight).
920 ℃ of carburizing temperatures, 4 hours time
Carburizing treatment grade of steel: 20CrMnTi 15 #Steel 12CrNi 3
Alloying layer thickness: 1.1mm(20CrMnTi)
0.65mm(15 #Steel)
0.94mm(12CrNi 3
Back hardness: the HRC58 of the oil (No. 20 machine oil) of quenching~60
Cementing furnace: RJJ-60
Drip amount: 130 droplets/minute of methyl alcohol
Oxygen probe is visited gesture control accuracy≤0.05%
Embodiment 4:
Complex carburizer with the present invention, contain kerosene 78%, n-propyl alcohol 20%, Pentyl alcohol 1.7% and rare earth element 0.3%(be % by weight all), with it earlier in pyrolyzer, cracking under 920 ℃ of cracking temperatures, deliver in the ZDJ-1000 ion carburizing vacuum furnace 1000 ℃ of carburizing temperatures, time hour after by 1: 2 mixed with nitrogen, the grade of steel of carburizing treatment is 20CrMnTi, alloying layer thickness 1.125mm.
The packing of complex carburizer of the present invention, sign, storage, transportation, acceptance of delivery etc. are all by ZBJ36.

Claims (3)

1, a kind of complex carburizer is characterized in that by the kerosene that dissolves each other, and pure and mild rare earth element is formed, and wherein contains kerosene 60~80%, alcohols 20~40% and rare earth element 0.3~0.6% (all %) by weight.
2,, it is characterized in that said pure carbon atom quantity preferably 1~7 according to the described complex carburizer of claim 1.
3,, it is characterized in that said rare earth element preferably cerium and/or lanthanum according to the described complex carburizer of claim 1.
CN88107570A 1989-03-04 1989-03-04 Composite carburizing agent Expired CN1010788B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN88107570A CN1010788B (en) 1989-03-04 1989-03-04 Composite carburizing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN88107570A CN1010788B (en) 1989-03-04 1989-03-04 Composite carburizing agent

Publications (2)

Publication Number Publication Date
CN1036232A true CN1036232A (en) 1989-10-11
CN1010788B CN1010788B (en) 1990-12-12

Family

ID=4854189

Family Applications (1)

Application Number Title Priority Date Filing Date
CN88107570A Expired CN1010788B (en) 1989-03-04 1989-03-04 Composite carburizing agent

Country Status (1)

Country Link
CN (1) CN1010788B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003006700A1 (en) * 2001-07-09 2003-01-23 Langen Li Atmosphere heat treatment cocatalyst, method of its application, heat treatment method and heat treatment atmosphere of using the cocatalyst
CN103757584A (en) * 2014-01-27 2014-04-30 内蒙古科技大学 Preparation method of rare earth carburized wear-resistant Fe-W alloy
CN103757583A (en) * 2014-01-27 2014-04-30 内蒙古科技大学 Preparation method for surface-strengthened Fe-W alloy
CN105483604A (en) * 2015-12-30 2016-04-13 武汉材料保护研究所 Catalytic permeation method for increasing austenite stainless steel low-temperature gas carburizing speed
CN113943161A (en) * 2021-11-25 2022-01-18 王耀民 Ti (BCN) powder and preparation method thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003006700A1 (en) * 2001-07-09 2003-01-23 Langen Li Atmosphere heat treatment cocatalyst, method of its application, heat treatment method and heat treatment atmosphere of using the cocatalyst
CN103757584A (en) * 2014-01-27 2014-04-30 内蒙古科技大学 Preparation method of rare earth carburized wear-resistant Fe-W alloy
CN103757583A (en) * 2014-01-27 2014-04-30 内蒙古科技大学 Preparation method for surface-strengthened Fe-W alloy
CN103757583B (en) * 2014-01-27 2015-12-09 内蒙古科技大学 A kind of preparation method of surface strengthened Fe-W alloy
CN103757584B (en) * 2014-01-27 2016-08-17 内蒙古科技大学 A kind of preparation method of rare earth catalytic cementation surface abrasion resistance Fe-W alloy
CN105483604A (en) * 2015-12-30 2016-04-13 武汉材料保护研究所 Catalytic permeation method for increasing austenite stainless steel low-temperature gas carburizing speed
CN105483604B (en) * 2015-12-30 2018-02-13 武汉材料保护研究所 A kind of raising austenitic stainless steel cryogenic gas carburizing speed urges infiltration method
CN113943161A (en) * 2021-11-25 2022-01-18 王耀民 Ti (BCN) powder and preparation method thereof

Also Published As

Publication number Publication date
CN1010788B (en) 1990-12-12

Similar Documents

Publication Publication Date Title
Patscheider et al. Structure–performance relations in nanocomposite coatings
Dumoulin et al. Role of molybdenum in phosphorus-induced temper embrittlement
Christensen et al. Microzonation of denitrification activity in stream sediments as studied with a combined oxygen and nitrous oxide microsensor
GB1562739A (en) Atmosphere compositions and methods of using same for surface treating ferrous metals
ES2043826T3 (en) METHOD FOR DEPOSITION OF INCREASED SILICON OXIDE IN PLASMA.
Welsh et al. Denitrification in an intertidal seagrass meadow, a comparison of 15 N-isotope and acetylene-block techniques: dissimilatory nitrate reduction to ammonia as a source of N 2 O?
CN1036232A (en) A kind of complex carburizer
CA2079978A1 (en) Vapour phase carbon deposition process for metal part surfaces and part thus obtained
CN1521221A (en) a protective coating
Costa et al. Effect of hydrogen incorporation on the mechanical properties of DLC films deposited by HiPIMS in DOMS mode
CN102125862B (en) Low-temperature carbonitriding catalyst and carbonitriding method thereof
AU635868B2 (en) Process for the production of a controlled atmosphere for heat treatment of metals
JP2000144391A (en) Sliding member
JP3824199B2 (en) Sliding member
Chen et al. The morphology and mechanical properties of TiN/Ni–P–SiC hybrid coatings
Saunders et al. Behaviour of Fecralloy and Iron Aluminides Alloys in Coal Gasification Atmospheres Containing HCI
CN1189547C (en) Synthetic diesel oil
Xiong et al. Research on high-temperature oxidation resistance, hot forming ability, and microstructure of Al–Si–Cu coating for 22MnB5 steel
Savitskii et al. Physico-chemical research in noble metals
Jinchang et al. Effect of different defocus distance on semiconductor laser nitriding of TC4 titanium alloy
Schulz et al. Factors affecting cyclic lifetime of EB-PVD thermal barrier coatings with various bond coats
CN1025226C (en) Rare earth catalytic ion S, N, C co-osmosizing agent and its technology
JP2019151913A (en) Sliding member and method for manufacturing the same
Makowski et al. Diesel‐lubricated ta‐C coatings
Maslyuk et al. Wear-resistant and corrosion-resistant carbide-steel-type materials having different matrices

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C13 Decision
GR02 Examined patent application
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee